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Recent Progress in Electroless Plating of Copper

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In this article, the recent developments in electroless plating of copper, electroless bath formulation and effect of plating parameters have been reviewed. Cyanide free electroless baths are now being developed and studied due to the various environmental concerns. Various organic chemicals such as complexing agents, reducing agents, and additives such as poly-alcohols and aromatic ring compounds have been added to copper plating baths for promising results. The effects of various reducing and complexing agents, bath conditions like additives, bath pH, and composition have been summarized. Finally the applications of the electroless plating of copper and latest developments have been overviewed for further guidance in this field.
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J. Microelectron. Packag. Soc., 23(4), 1-6 (2016) https://doi.org/10.6117/kmeps.2016.23.4.001
Print ISSN 1226-9360 Online ISSN 2287-7525
1
Recent Progress in Electroless Plating of Copper
Ashutosh Sharma1, Chu-Seon Cheon2 and Jae Pil Jung1,
Dept. of Materials Science and Engineering, University of Seoul, 163, Seoulsiripdae-ro, Dongdaemun-gu, Seoul 02504, Korea
Danyang Soltec Co. Ltd., 29, Mado-ro 660beon-gil, Mado-myeon, Hwaseong-si, Gyeonggi-do 18541, Korea
(Received December 9, 2016: Corrected December 12, 2016: Accepted December 14, 2016)
Abstract: In this article, the recent developments in electroless plating of copper, electroless bath formulation and effect
of plating parameters have been reviewed. Cyanide free electroless baths are now being developed and studied due to
the various environmental concerns. Various organic chemicals such as complexing agents, reducing agents, and additives
such as poly-alcohols and aromatic ring compounds have been added to copper plating baths for promising results. The
effects of various reducing and complexing agents, bath conditions like additives, bath pH, and composition have been
summarized. Finally the applications of the electroless plating of copper and latest developments have been overviewed
for further guidance in this field.
Keywords: Electroless, additives, plating, copper, complexing agents, temperature
1. Introduction
Electroless plating is known for hundreds of years. It is a
process of deposition of thin layer of metals, salts, oxides
and other compounds used in various industrial and tech-
nological applications. The deposition of precious metals
like gold and silver were already used in early civilizations.
Wurtz in 1844 discovered the first nickel electroless coat-
ing using hypophosphite as a reducing agent. Later in
1946, Brenner and Riddell developed the process and pro-
posed the operating conditions for the nickel electroless
plating. They included various reducing agents including
sodium hypophosphite to obtain a controlled nickel plating.
William Blum coined the term ‘Electroless’ for this auto-
catalytic process because of no need of supplying external
current into the electrolyte bath.1) In electroless technique,
a noble metal is deposited from its salt on a catalytic active
surface of a less noble metal. On the contrary the electro-
plating involves supply of an external current for reaction
to happen. Apart from composition and organic additives,
electroplating involves a number of parameters like cur-
rent, pulse type, frequency and duty cycle of pulse, etc.,
making the process more complex.2-7) While in electroless,
the reaction is catalyzed by employing a suitable reducing
agent which supplies the electron for reduction reaction
and metal is deposited over the substrate.1,8) The reactions
can be shown as below:
Metal ion (M+) + Reducing agent (Red)
Metal Deposited + Oxidized product (Ox) (1)
There are two reactions in electroless plating:
Metal deposition: M+ + e M (1a)
Oxidation: Red + H2O Ox + H+ + e (1b)
Here, M: Metal, e: electron, Red: Reducing agent, Ox:
Oxidized product
The process is electrolytic as well as electroless in nature
as shown in Fig. 1.
The thickness of electroless coatings can reach up to 10
to 200 µm. Electroless plating is more useful than electro-
plating, for example, the possibility of producing coatings
with uniform thickness, depositing material even in deep
recess/vias, ability to produce very thin layers, excellent
step coverage, independent of the sizes, shape or conduc-
tivity of the substrate and absence of need for electrical
contacting of wafers during deposition.9,10) Significant
advancement occurred in electroless plating of Cu, Ni, Au,
Ag, Pd, Sn, etc., for industrial applications, however, the
various operating parameters and bath conditions are not
fully understood.10)
Corresponding author
E-mail: jpjung@uos.ac.kr
©
2016, The Korean Microelectronics and Packaging Society
This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License(http://creativecommons.org/
licenses/by-nc/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is
properly cited.
특집
:
Electroless Plating of Copper
2Ashutosh Sharma, Chu-Seon Cheon and Jae Pil Jung
마이크로전자 패키징학회지 23 4 (2016)
2. Electroless Copper Plating
Copper is one of the oldest element known in the history.
In Latin, copper is termed as cuprum the Iceland of Cyprus
dates back to 11000 years.11) In the late 18th century, cop-
per was picked up by many scientists like Ampere, Fara-
day and Ohm for their discoveries in electricity and mag-
netism. Pure copper is soft, malleable and ductile with very
high thermal and electrical conductivity.10,11) Electroless
copper coatings provide protection for common metal sur-
face exposed to corrosion and wear. Electroless copper is
the material of today. As a coating, it is used in several
industrial applications ranging from aerospace, automotive,
electronics, telecommunications, information technology,
food processing, beauty care products, nuclear engineering,
petrochemicals, plastics, power transmission, printing,
pump valves, textiles etc..12) Electroless copper is being
extensively used in microelectronics and packaging of
devices, for interconnects in ultra large scale integration
(ULSI), IC fabrication and EMI shielding because it
doesn’t require vacuums or high temperature for thin metal
film deposition due to their high conductivity, resistance to
electro migration and no requirement for vacuum and high
temperature.10-12)
3. Plating Baths
3.1. Traditional baths
Traditional electroless plating baths are based on reduc-
ing agents based on formaldehyde and its derivatives. This
type of baths have two major drawbacks, such as, (1) form-
aldehyde baths operates around alkaline pH values
(> 11).10,13) (2) Aldehydes are volatile, flammable and pose
health hazard to human beings. Aldehydes have significant
environmental impact and continuous exposure to formal-
dehyde causes severe skin rashes, eye infections, difficulty
in coughing and breathing.10-14)
To overcome these drawbacks, people have used many
electroless copper baths based on non-formaldehyde
chemicals, e.g., hypophosphite, sodium bisulfate (NaH-
SO3), glyoxylic acid, the sodium thiosulfate pentahydrate
(Na2S2O3·5H2O), borane-dimethylamine complex, Co(II),
Fe(II),15-23) etc. Sodium hypophosphite is most attractive
due to its excellent bath stability, easy control, and lower
cost. However, the hypophosphite may oxidize on prolong
storage and may lead to the reduction in deposit quality.
For, alkaline baths the oxidation of hypophosphite can be
minimized by the addition of catalytic ions like Ni2+ or
Pd2+ ions.19,21-24) This increases the efficiency of the pro-
cess but limits the conductivity of the deposits due to the
impurities of Ni and Pd incorporated.19)
3.2. Methyl sulphonic acid (MSA) baths
MSA baths are getting more attention in the formulation
of electrolytic baths in electroless as well as electroplating
deposition of metals. MSA is the reducing acid which min-
imizes the oxidation of the metal ions. Procell et al. discov-
ered that alkyl sulphonic acids form highly soluble metal
salts in water producing clear solutions.24) MSA based
baths become popular during 1980’s for different metal
plating baths and is an excellent choice for various plating
applications.1,8-11,25,26) MSA acid is a transparent liquid hav-
ing chemical formula CH3SO3H characterized by
(i) Transparent slight yellowish
(ii) Soluble in water and sparingly soluble in benzene
(iii) Insoluble in paraffins
(iv) High conductivity better than HCl and H2SO4
(v) Excellent stability
(vi) Less toxic and safe to handle
(vii) Biodegradable, easy disposal
The deposits produced from MSA baths are of high qual-
ity, high adhesion strength, smooth free from dendrites and
porosity. The superiority of MSA over other plating baths
arises due to the fact that it can be operated at room tem-
perature, excellent bath life and conductivity, and bio-
degradability.25,26)
3.3. Complexing Agents
The complexing agents in electroless copper baths are
very important for good quality deposits. Complexing agents
minimize the formation of copper to copper hydroxides
(Cu(OH)2) in alkaline pH range.17) Complexing agents sta-
Fig. 1. Schematic representation of electroless metal deposition.
Recent Progress in Electroless Plating of Copper 3
J. Microelectron. Packag. Soc. Vol. 23, No. 4 (2016)
bilized the baths and increases bath life. Addition of com-
plexing agents in a small quantity increases in plating rate.
The mixed potential theory of electroless plating states that
the overall reaction of the electroless copper process is
given by two following half-reactions:
Cathodic reaction:
Cu[L]x +2 +2e
→ Cu + xL (2)
Anodic reaction:
2HCHO + 4OH → 2HCOO + H2 + 2H2O + 2e
(3)
During the electroless process, the two reactions occur
simultaneously on a catalytic surface. The most common
complexing agents for electroless copper are Ethylenedi-
aminetetraacetic acid (EDTA), trisodium citrate, malic
acid, lactic acid, triethanolamine, sodium potassium tarta-
rate, etc..27-30) EDTA and sodium potassium tartrate have
been used extensively in traditional electroless copper
baths containing formaldehyde as a reducing agent. These
plating baths produce low plating rates due to the forma-
tion of the cupric complexes and the shift in reduction
potential toward negative values. Moreover, EDTA is non-
biodegradable and produces serious waste disposal prob-
lems.31) In last few decades, the use of Triethanolamine
(TEA) has been used to yield higher plating rates com-
pared to when using EDTA.32) However, high plating rates
are associated with poor bath stability and deposit quality.
Tartrate based chelates are used for low plating rate at low
temperature. Tartrates are easy to dispose during waste
treatment but are not suitable for high speed plating pro-
cesses. Other biodegradable chelating agents are polyols.
Polyols easily form chelates with Cu(II) ions in alkaline
medium. The examples include glycerol, xylitol, sacchar-
ose, alditol, erythritol, adonitol, D-mannitol, D-sorbitol,
maltitol, lacticol etc., for eco-friendly chelating agents for
alkaline electroless plating.33)
3.4. Reducing Agents
The role of reducing in electroless plating is most
important as it reduces the cupric ions (Cu2+) to metal
atoms copper (Cu) without any change to cuprous oxide
(Cu+). Traditional electroless copper plating baths often
use formaldehyde as the reducing agent.13) While using
formaldehyde, the electroless copper deposition can be rep-
resented as:
Cu2+ + 2HCHO- + 4OH-
→ Cu + 2HCOO- +2H2O +H2 (4)
However, formaldehyde is not completely effective in
alkaline pH values due to oxidation of the plating bath.14)
In addition, formaldehyde is volatile and toxic in nature.
Non-formaldehyde reducing agents used currently include,
glyoxylic acid], hypophosphite], sodium bisulfate (NaH-
SO3), sodium thiosulfate pentahydrate (Na2S2O3,5H2O),
Co(II),46) Fe(II) etc.16-22,27-32) Sodium hypophosphite is the
most popular reducing agent used in copper electroless
bath due to its low price, bath stability, and relatively easy
to control plating conditions.34) The electroless copper plat-
ing reaction using hypophosphite is given:
Cu2+ + 2H2PO2
+ 2 OH- → Cu+ 2H2PO3- + H2 (5)
The catalytic activity of hypophosphite is weaker and
therefore the substrate must be prior activated with Pd or
Ni ions.17,19)
Glyoxylic acid as an alternative reducing agent for elec-
troless copper plating has been used by various researchers.
Glyoxylic acid provides higher plating rates and bath sta-
bility compared to that with formaldehyde reductant.14,15,35)
The overall reaction with glyoxylic acid is:
Cu2+ + 2CHOCOOH + 4OH-
→ Cu + 2HC2O4- + 2H2O +H2 (6)
CHOCOOH + 3OH-
→ HC2O4
+ 2H2O + 2e- + 1.01V/SHE (7)
This reaction is commonly accompanied by the Canniz-
zaro reaction,
2CHOCOOH + 2OH-
→ C2O42
+ HOCH2COOH + H2O (8)
Other reducing agents investigated in electroless deposi-
tion of copper are Dimethylamine borane (DMAB), hydra-
zine, aminoborane and phenylhydrazine, but their applications
are limited due to bath stability and deposit quality optimi-
zations.22,36-38)
3.5. Additives
The additives are generally used to prevent decomposi-
tion of electroless baths. They behave as bath stabilizers.
Additives also affects the physical and mechanical proper-
ties of the deposit.27,38-40) There are various kinds of addi-
tives in electroless plating:
(a) Inhibitors: They are used to increase the throwing
power into holes and recess. e.g., polyethers or polyoxy-
ethers.
(ii) Levelers: Levelers improve plating thickness unifor-
mity at corners and projections and levels the plated layer,
e.g., amines, amide surfactants.
4Ashutosh Sharma, Chu-Seon Cheon and Jae Pil Jung
마이크로전자 패키징학회지 23 4 (2016)
(iii) Brighteners: Brighteners control deposit brightness
and hardness. They attach to the copper metal ions during
plating and facilitate charge transfer at the electrode.
Brighteners accelerate plating rates and also control grain
structure and deposit characteristics, e.g., Sulphur contain-
ing compounds.
(iv) Wetting agents: They decrease surface tension in
solution. Surfactants lower the surface tension of the plat-
ing solution and thus, allow better wetting of the electro-
lyte at the electrode.
The common additives in copper electroless plating baths
include thiourea, pyridine, cytosine, glycine, guanine, ade-
nine, guanine, ammonia, sodium dodecyl sulphate (SDS),
polyethylene glycol (PEG), mercapto group compounds,
benzo triazole (BTA), di-pyridyl etc. The additives are ben-
eficial in modifying crystal size, shape and orientation, and
adherent copper deposits.1,8-10,13-23)
3.6. Bath pH
Bath pH is an important parameter in electroless deposi-
tion. Bath pH controls the plating rate, microstructure, sur-
face roughness and the crystallinity of the coating.41)
Whenever there is an oxidation of the reducing agents, it
indicates the formation of hydrogen or hydroxyl ions
(OH
). The bath pH should be stable for better efficiency
of the process. A change in pH severely affects the deposi-
tion rate during plating and hence the mechanical proper-
ties can get affected. To overcome unstable bath pH values,
various stabilizers such as NaOH, KOH, carboxylic acids
and amines are used in alkaline solutions.
4. Applications of Copper Electroless Plating
Last few decades have seen enormous growth and demand
of electroless copper plating in microelectronics packaging,
aerospace, automotives industries, etc. In advanced 3D
packaging technology, copper electroless plating is the
material of choice. Recently, electroless copper has been
tried for the functionalization of nanostructured materi-
als.13,14) Production of copper nano particles using hydra-
zine as reducing agent that have also been tried. Not only
metallic but also ceramics and polymers have been coated
with electroless copper in various engineering applica-
tions.13) Copper plating on polyamides, acrylonitrile butadi-
ene styrene, polyethylene terephthalate, polypropene, teflon,
films are flexible and used in modern flexible stretchable
electronics, PCBs and shielding applications.18)
Lightweight composites using the electroless copper
plating method. The pollen grains of the lightweight flow-
ers have been coated with copper electroless coating using
Pd catalyst.42,43) Substrates in solder joints for electronics,
multilayer boards via plated through-hole technique is per-
formed using electroless copper plating.44) Copper plated
ceramics are employed in microwave circuits in radar, tele-
communication and in spacecraft. Electroless plating is
important for various processes in electronic, computer,
and metallurgy industry of today.45,46)
5. Conclusion
The process of electroless copper coating on a substrate
is an autocatalytic reduction process. Copper electroless
plating uses a chemical bath composed of complexing
agents, reducing agents like hypophosphite and various
organic additives for better surface finish. The electroless
copper process has been successfully applied to various
surface protection, decorative, electronics, computers, infor-
mation technology, telecommunications and satellites. Elec-
troless copper applied on non-conducting base are used in
wide range of applications in modern flexible electronic
devices and sensors. It is concluded that a good fundamen-
tal background of copper electroless plating is needed to
understand the various roles of organic components in
electroless plating baths so that the properties of copper
coatings can be further improved considerable. This will
set a new direction for electroless plating in the modern
research community.
Acknowledgements
This work (Grants No. C0398999) was supported by
Business for Cooperative R&D between Industry, Acad-
emy and Research Institute funded Korea Small and
Medium business Administration in 2016.
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Ashutosh Sharma
Department of Materials Science and
Engineering, University of Seoul, Seoul-
02504, South Korea
Research Interests: Pulse Electroplating,
Lead Free Soldering, Brazing, Metal Matrix
Nanocomposites
Email: stannum.ashu@gmail.com
Chu-Seon Cheon
Danyang Soltec Co. Ltd., Hwaseong-si,
Gyeonggi-do, 445-861, Korea
Research Interests: Solder Pastes, Lead Free
Soldering
E-mail: zeuscheon@dyst21.co.kr
Jae Pil Jung
Department of Materials Science and
Engineering, University of Seoul, Seoul-
02504, South Korea
Research Interests: Microjoining,
Electroplating, Brazing Fillers, Solder-Joint
Reliability, Metal Matrix Nanocomposites,
Lead Free Soldering
... Classical chemical processes of copper plating [34,35] are widely used in the production of various types of nanoscale materials [36]. In previous studies, various types of reducing agents, such as formaldehyde [35], ascorbic [37,38] or glyoxylic [31,39,40] acid, hydrazine hydrate [41], hypophosphite [42], dimethylamine borane [43,44], etc., were used in copper deposition solutions. ...
... Classical chemical processes of copper plating [34,35] are widely used in the production of various types of nanoscale materials [36]. In previous studies, various types of reducing agents, such as formaldehyde [35], ascorbic [37,38] or glyoxylic [31,39,40] acid, hydrazine hydrate [41], hypophosphite [42], dimethylamine borane [43,44], etc., were used in copper deposition solutions. At room temperature, the reduction reaction of copper(II) ions is possible only when using formaldehyde as a reducing agent, but its high toxicity limits the use of this composition for coatings used in pharmaceuticals and biomedicine [45]. ...
... It can be seen that composites obtained using DMAB as a reducing agent have the least activity in the decomposition reaction of Cr(VI) ions, which is most likely due to the presence of the copper(I) oxide phase in the composite [27]. The Cr(VI) chromium ion decomposition reaction proceeds according to the Langmuir-Hinshelwood mechanism and has a pseudo-first order [35], which makes it possible to calculate the rate constant by changing the concentration of the key component (Fig. 5b). The calculated value of the reaction rate constant k a for composites of the Cu_DMAB@PET com- position (0.017 min -1 ) is more than 9 times less than that of composites obtained using glyoxylic acid (0.156 min -1 ) and more than 15 times less than the k a value of Cu_CHOH@PET samples (0.249 min -1 ). ...
Article
Full-text available
The features of obtaining composite track-etched membranes based on copper microtubes using various com-positions of a deposition solution and various types of reducing agents such as formaldehyde (Cu_CHOH@PET), dimethylamine borane (Cu_DMAB@PET), glyoxylic acid (Cu_Gly@PET) were studied in this research. The structure and composition of the membrane composites were studied by scanning elec-tron microscopy and X-ray phase analysis. It was shown that in the case of using dimethylamine borane as a reducing agent, the obtained composites consisted of copper(I) oxide (37.4 %) and copper(0) (62.6 %), in other cases single-component copper microtubes were obtained. The reduction reaction of chromium(VI) ions was used in order to evaluate the catalytic ability of prepared composites. It was shown that the removal effi-ciency of chromium ions reached up to the 95–97 % in the case of single-component composites; the pres-ence of a copper(I) oxide phase in the structure of the Cu_DMAB@PET composites significantly reduced the activity of catalysts and under similar conditions only 41% of the contaminant was removed from the reaction system. The degradation reaction of Cr(VI) was found to follow the Langmuir-Hinshelwood mechanism and a pseudo-first-order kinetic model. The calculated value of the reaction rate constant ka for composites of the Cu_DMAB@PET composition (0.017 min–1) was more than 9 times less than that of composites obtained us-ing glyoxylic acid (0.156 min–1) and more than 15 times less than the ka value of Cu_CHOH@PET samples (0.249 min–1). Effect of temperatures on the catalytic ability of composites was studied in the temperature range of 10–38 °C. Some thermodynamic characteristics such as activation energy, enthalpy and entropy of activation were calculated. It was found that the minimum value of the activation energy was obtained for the Cu_CHOH@PET samples.
... Formaldehyde is inexpensive and has a high oxidation rate; however, it has a strong odor and adverse effects on the human body and environment. [26,27] In this study, glyoxylic acid (CHOCOOH) was used as a reducing agent; it has a high Cu deposition rate, no irritating odor, and is easier to handle. [27][28][29][30][31][32][33] Cu is deposited on PGM particles in the washcoat of the autocatalyst, which have catalytic activity for glyoxylic acid; however, Cu is not deposited on ceramic components with no catalytic activity. ...
... [26,27] In this study, glyoxylic acid (CHOCOOH) was used as a reducing agent; it has a high Cu deposition rate, no irritating odor, and is easier to handle. [27][28][29][30][31][32][33] Cu is deposited on PGM particles in the washcoat of the autocatalyst, which have catalytic activity for glyoxylic acid; however, Cu is not deposited on ceramic components with no catalytic activity. ...
Article
Full-text available
Platinum group metals (PGMs) are primarily used in automotive exhaust catalysts (autocatalysits). Spent autocatalysts are the most important secondary resource for PGMs. However, transporting autocatalyst scraps and recovering PGMs from the scraps are costly and time-consuming, owing to the low PGM content in spent autocatalysts. Thus, an effective PGM-concentration technology for the pretreatment of scrap prior to transport is required. This study develops a new pretreatment technique that is applied prior to the flotation concentration of PGMs in autocatalysts. This method utilizes electroless Cu plating followed by sulfurization. In the electroless Cu-plating process, which uses glyoxylic acid as a reducing agent, Cu is deposited on the PGM particles in the washcoat of the autocatalyst. During the sulfurization process, S vapor sulfurizes the deposited Cu into copper sulfide, which is hydrophobic. Prior to the experiments, thermodynamic considerations were made to predict the reactivity of Cu and the representative elements constituting the autocatalyst with S vapor, and the sulfurization conditions were designed. Sulfurization experiments were performed at 850 K (577 °C) in the presence of carbon (C), and the results show the successful conversion of only Cu to copper sulfide without sulfurizing the representative oxides (MgO, Al 2 O 3 , SiO 2 , CeO 2 , and ZrO 2 ) present in the autocatalyst. Finally, in the flotation process, the copper sulfide-coated PGMs are separated from the ceramic components of the autocatalyst, which is hydrophilic; thus, it is concentrated in the froth. Flotation experiments utilizing a microbubble flotation method were successfully performed to recover the PGM concentrates. This innovative pretreatment technique is expected to reduce the cost and time required for the entire PGM recycling process.
... Electroless plating is a type of surface treatment in which a thin layer of metals, salts or other compound is plated without the use of external power. This electrochemical deposition occurs as a result of a redox reaction between the metal and the reducing agent for e.g., hypophosphite, leading to the reduction and subsequent deposition of metallic ions on to the surface [76][77][78][79][80]. The wide application of electroless plating is due to the uniformity regardless of the shapes and size of the surface, low porosity and roughness, high adhesion of these coatings to the substrate and the excellent corrosion, wear and abrasion and fouling resistance [80,81]. ...
... This electrochemical deposition occurs as a result of a redox reaction between the metal and the reducing agent for e.g., hypophosphite, leading to the reduction and subsequent deposition of metallic ions on to the surface [76][77][78][79][80]. The wide application of electroless plating is due to the uniformity regardless of the shapes and size of the surface, low porosity and roughness, high adhesion of these coatings to the substrate and the excellent corrosion, wear and abrasion and fouling resistance [80,81]. Cheng, Y., et al. [82] investigated the anti-fouling properties of Ni-P electroless plating on low-carbon steel under various operating conditions. ...
Preprint
Full-text available
Geothermal energy is likely to be a significant contributor in achieving sustainable energy goals and net-zero emissions targets. Within geothermal power plants, heat exchangers play a critical role in harnessing this renewable energy source. However, these heat exchangers encounter significant challenges when exposed to geothermal fluids, including erosion, corrosion, and scaling, which adversely affects their performance and longevity. The current review focuses on surface engineering techniques, particularly coatings, as a highly effective and economically viable solution to address these challenges in geothermal heat exchangers. The review begins by providing an overview of geothermal energy, its significance in the context of sustainability and the important role played by heat exchangers in geothermal power generation, followed by the challenges and their impact on heat exchangers. The subsequent section focuses on surface engineering by coatings and its types employed to enhance the performance of heat exchangers. In the final part, the reader is presented with an overview of the challenges associated with the application of coatings in geothermal heat exchangers and potential future directions in this field. This review offers a detailed understanding of the critical role coatings play in improving the efficiency and service life of heat exchangers in geothermal power plants.
... Классические процессы химического меднения [1,2] широко используются в процессах синтеза наночастиц (НЧ) меди, а также полых нанотрубок (НТ) по технологии темплатного химического синтеза (англ.: electroless template synthesis) [3] с использованием шаблонных матриц различной природы: пористых полимерных трековых мембран (ТМ) [4,5], анодированной окиси алюминия [6], углеродных НТ [7] и волокон [8]. В литературе встречаются данные об использовании различных восстановителей темплатного ХО меди: формальдегид [2], аскорбиновая [9,10] или глиоксиловая [11][12][13] кислоты, гидразингидрат [14], гипофосфит [15] и диметиламин-боран [16,17] и др. ...
... Классические процессы химического меднения [1,2] широко используются в процессах синтеза наночастиц (НЧ) меди, а также полых нанотрубок (НТ) по технологии темплатного химического синтеза (англ.: electroless template synthesis) [3] с использованием шаблонных матриц различной природы: пористых полимерных трековых мембран (ТМ) [4,5], анодированной окиси алюминия [6], углеродных НТ [7] и волокон [8]. В литературе встречаются данные об использовании различных восстановителей темплатного ХО меди: формальдегид [2], аскорбиновая [9,10] или глиоксиловая [11][12][13] кислоты, гидразингидрат [14], гипофосфит [15] и диметиламин-боран [16,17] и др. При комнатной температуре реакция восстановления ионов меди (II) возможна лишь при использовании формальдегида в качестве восстановителя. ...
Article
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The kinetic and thermodynamic parameters of the decomposition of an inorganic wastewater pollutant such as potassium hexacyanoferrate (III) (PHCF) in the presence of composite catalysts based on polymer track membranes (TeMs) and copper nanoparticles (NPs) was studied. Composite catalysts were prepared by electroless template synthesis using a nontoxic reducing agent - ascorbic acid. A systematic study of the process of electroless plating of copper NPs was carried out depending on pH, deposition time, and the number of activations of the polymer template. The structure of the porous composite catalysts was investigated by scanning electron microscopy and X-ray diffractometry. The catalytic properties of the obtained composites were examined in the temperature range of 10-25 °C for a series of samples synthesized with different deposition times. It was shown that the kinetics of the decomposition reaction of PHCF corresponds to the pseudo first-order reaction. Such thermodynamic characteristics as energy, entropy and enthalpy of activation are calculated. The stability of the properties of catalysts has been studied.
Article
The production of complex structures out of a variety of materials has undergone a revolution due to the rapid development of additive manufacturing (AM) technology. Initially confined to applications such as magnetic actuators and two-dimensional electric or electronic circuits, the convergence of 3D printing and metallization methods has emerged as a revolutionary approach. This synergy facilitates the creation of functional and customizable metal-polymer hybrid structures characterized by high strength, lightweight properties, intricate geometric designs, and superior surface finish. These structures also exhibit enhanced electrical and thermal conductivity, as well as optical reflectivity. This paper reviews techniques to improve the effectiveness of 3D-printed polymer antennas and structures by using various techniques of metallization. The metallization processes are examined, and a classification based on the materials employed is presented to facilitate comparisons that highlight the optimal utilization of materials for the fabrication of 3D-printed polymer structures. The main emphasis here is on the effectiveness of different processes in terms of deposition, bonding strength, electrical conductivity, and various characteristics of metallic coatings developed on polymers. This review contributes an in-depth analysis of the latest developments in 3D printing and metallization techniques specifically applied to polymer antennas and structures. The exploration extends to potential applications, challenges encountered, and future prospects within this dynamic field. As AMandmetallization continue to evolve, this study aims to provide a comprehensive understanding of the state-of-the-art methodologies and their implications for the future of polymer-based structures and antennas.
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Full-text available
Geothermal energy is likely to be a significant contributor in achieving sustainable energy goals and net-zero emissions targets. Within geothermal power plants, heat exchangers play a critical role in harnessing this renewable energy source. However, these heat exchangers encounter significant challenges when exposed to geothermal fluids, including erosion, corrosion, and scaling, which adversely affects their performance and longevity. The current review focuses on surface engineering techniques, particularly coatings, as a highly effective and economically viable solution to address these challenges in geothermal heat exchangers. The review begins by providing an overview of geothermal energy, its significance in the context of sustainability and the important role played by heat exchangers in geothermal power generation, followed by the challenges and their impact on heat exchangers. The subsequent section focuses on surface engineering by coatings and its types employed to enhance the performance of heat exchangers. In the final part, the reader is presented with an overview of the challenges associated with the application of coatings in geothermal heat exchangers and potential future directions in this field. This review offers a detailed understanding of the critical role coatings play in improving the efficiency and service life of heat exchangers in geothermal power plants.
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Full-text available
A microchannel heat sink integrated with a three-dimensional manifold using Direct Bonded Copper (DBC) is promising for high power density electronics due to the combination of low thermal resistance and reduced pressure drop. However, this requires much progress on the fabrication and high-quality point-contact bonding processes of the microchannel substrate and 3D manifold DBCs. In this study, we have developed processing techniques for surface preparations and high-quality point-contact solder bonding between the two DBC substrates. We utilized chemical polishing followed by electroless plating to prevent excess solder from blocking the microchannels. We performed a parametric study to investigate the impact of bonding time and surface roughness on the tensile strength of the bonding interface. The bonding strength increased from 1.8 MPa to 2.3 MPa as the bonding time increased from 10 to 30 minutes while reducing the surface roughness from Rz = 0.21 to 0.05 µm, resulting in increasing the bonding strength from 0.16 MPa to 2.07 MPa. We successfully tested the microcooler up to the inlet pressure of 70 kPa and pressure drop of 30 kPa, which translates to the tensile strength at the bonding point contacts, which remains well below the 2.30 MPa. We achieved the junction-to-coolant thermal resistance of 0.2 cm2-K/W at chip heat flux of 590 W/cm2. Thus, our study provides an important proof-of-concept demonstration towards enabling high power density modules for power conversion applications.
Article
To separate both copper and 2,2',2'',2'''-(ethane-1,2-diyldinitrilo)tetraacetic acid (EDTA) from the waste electroless copper plating solution by solvent extraction, the liquid–liquid equilibria of the copper-EDTA complex and unbound EDTA ion were experimentally measured. An organic solution of tri-n-octylmethylammonium chloride (TOMACl) was used as solvent. The kerosene solution of TOMACl could extract both copper-EDTA complexes and EDTA ions from the model wastewater. The fractional removal and distribution ratios of both the copper-EDTA complex and EDTA ions decreased as the pH increased. The valence number of the major copper-EDTA complex or EDTA ion in the aqueous phase increased with pH, and the number of TOMA⁺ cations required to chelate the complexes and ions increased. These complexes and ions had lower reactivity with TOMACl owing to steric hindrance. These effects caused lower removal of both copper and EDTA in a higher pH range, which is a typical condition of waste electroless copper solution.
Article
The adsorption behavior of glycerol, erythritol, xylitol and glucose on copper surface was investigated via molecular dynamics simulation, in order to predict the effect of additive on throwing power of copper pyrophosphate bath, and then the electrochemical analysis was conducted to verify this prediction. The experimental data supported the simulation result, i.e., the pyrophosphate bath in presence of glycerol has the best throwing power. It is demonstrated that the molecular dynamics simulation is a promising tool with good accuracy for the additive screening in electroplating process.
Article
Two-step electroless process to form uniform deposition of Ir on Pt at various loadings. Creation of a functional multi-catalyst layer coated membrane (CCM).
Chapter
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In the electronic packaging industries, soldering materials are essential in joining various microelectronic networks. Solders assure the reliability of joints and protect the micro‐ electronic packaging devices. They provide electrical, thermal, and mechanical continuity among various interconnections in an electronic device. The service performance of all the electronic appliances depends on high strength and durable soldering materials. Lead-containing solders are in use for years, resulting in an extensive database for the re‐ liability of these materials. However, due to toxicity and legislations, lead-free solders are now being developed. As tin (Sn) is the major component of solders, this chapter presents the detailed results and discussion about the metallurgical overview of Sn, synthesis, and characterization of pulse electrodeposited pure tin finish from different aqueous solution baths. The experiments on pulse electrodeposition such as common tin plating baths em‐ ployed, their chemical compositions, rationale behind their selection and their characteri‐ zation by bath conductivity and cathodic current efficiency, microstructures, and tin whisker growth are discussed. Further, the effect of pulse electrodeposition parameters such as current density, additive concentration, pH, duty cycle, frequency, temperature, and stirring speed on microstructural characteristics of the coating obtained from sulfate bath and their effect on grain size distribution have been presented.
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The inhibitive behaviour of Vitamin C (ascorbic acid), as a type of green inhibitor, on the corrosive behaviour of stainless-steel (SS) X4Cr13 within an aqueous solution of hydrochloric acid (HCl) was studied within a concentration range of 0.01 - 5.0 M HCl. Potentiodynamic polarization and electrochemical impedance spectroscopy (EIS), was used for the measurements at 25 °C. The polarization curves revealed that the studied mixtures of the chosen inhibitor represented mixed-type of the inhibitor. A good inhibitive efficiency for Vitamin C at chosen concentration of 10-2 and 10-3 mol L-1 on the SS type X4Cr13 in HCl was limited to concentrations of HCl below 1.0 mol L-1.
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Full-text available
Pulse electrodeposition method is employed for the synthesis of Sn nanostructures using alumina template. Electrical contacts are made through metallisation of the template bottom with copper and an aluminium foil. The current density is varied from 0.05 to 0.6 A cm22, and a change in nanostructure formation is noticed. The structure and morphology of nanostructures are characterised by X-ray diffraction, field emission scanning electron microscopy and energy dispersive X-ray spectroscopy. It is observed that at a lower current density (0.05 A cm22), nanorods (mean diameter 186 nm) are prominent. As the current density is further increased to 0.4 A cm22, the nanorods increase in diameter (∼216 nm), while at a higher current density of 0.6 A cm22, nanorods (mean diameter 158), nanoribbons (mean diameter 126 nm) as well as nanowires (∼44 nm) are produced. The obtained Sn nanostructures are polycrystalline in nature and can be scaled up to industrial level.
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This study investigated the effect of heat treatment conditions not only on the Cr surface crack propagation behaviors but also on the Ni/Cr interfacial reaction characteristics in electroless Ni/electroplated Cr double coating layers on Cu substrate. Clear band layer of Ni-Cr solid solutions were developed at Ni/Cr interface after heat treatment at 750^{\circ}C for 6 h. Channeling cracks formed in Cr layer after 1 step heat treatment, that is, heat treatment after Ni/Cr plating, while little channeling cracks formed after 2 step heat treatment, that is, same heat treatments after Ni and Cr plating, respectively, due to residual stress relaxation due to crystallization of Ni layer before Cr plating.
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Die anodische Oxidation verschiedener Reduktionsmittel (NaH2PO2, CH2O, NaBH4, Dimethylaminboran und NHzNHz) wird an unterschiedlichen Metallelektroden (Au, Pt, Pd, Ag, Cu, Ni und Co) bei verschiedenen Temp. untersucht, wobei besonders der katalytische Aspekt der stromlosen Abscheidung von Interesse ist.
Book
Amorphous and Nano Alloys Electroless Depositions: Technology, Theory, Structure and Property describes the whole development and the most important subjects (technology, theory, structure and property) up to date of electroless plating (EP). The author concentrates on the fundamental scientific and academic problems (principle, mechanism and theory) in EP today. Based on the history of EP, this valuable reference describes lots of new EP processes, including electroless Fe based alloy system deposits, formation and theoretical description of electroless alloys, microscopic theory of electroless plating deposits, microscopic structures and surface morphology of electroless deposits, and weldability property of electroless deposits. • Focus on the fundamental scientific and academic problems (principles, mechanisms and theory) in electroless plating. • The book gives a very good overview of the research and development in this field and each chapter is fully referenced. • Detailed analysis and review of the current data, logically structured for ease of use. © 2016 Chemical Industry Press. Published by Elsevier Inc. under an exclusive license with Chemical Industry Press. All rights reserved.
Article
Electroless copper from solutions that contain glyoxylic acid as reducing agent formed a conformal thin film compatible with very large scale integrated technology for integrated circuits and microelectromechanical systems applications. Glyoxylic acid is an alternative reducing agent that can replace formaldehyde for basic copper sulfate based solutions without compromising thin film properties and process capabilities. Electroless copper was deposited on a silicon surface activated with palladium as well as on an oxide film activated by a thin layer of copper or cobalt. The resistivity of thin copper film, thicker than 300 nm, deposited from glyoxylic based solution was 2.3-2.4 mu Omega cm as deposited, and 1.9-2.0 mu Omega cm after a 200 degrees C anneal for 30 min. Thinner film resistivity increased as film thickness decreased following a simple power low. Electroless copper was deposited from solution with glyoxylic acid into via contact of 0.2 mu m diam and up to 4:1 aspect ratio. The deposit was smooth and conformal.
Article
A method for accelerating the deposition rate of electroless copper solutions is described which includes: 1. the addition (within optimum limits) of an accelerating agent selected from compounds containing a delocalized pi-bond; 2. the adjustment of solution pH to a value that maximizes the plating rate. The accelerating agents can be classified according to their capability to depolarize the cathodic and anodic partial reactions in formaldehyde-containing electroless copper baths.
Article
Description The papers in the Symposium on Metal Corrosion in the Atmosphere were given at the 70th Annual Meeting of the Society held at Boston, Mass., 25-30 June 1967. W. H. Ailor, Jr., Reynolds Metal Corp., and S. K. Coburn, U.S. Steel Corp., were the co-chairmen of this symposium sponsored by Committee G-1 on Corrosion of Metals.